FI955775A0 - Multiphase stage passive reactor - Google Patents

Multiphase stage passive reactor

Info

Publication number
FI955775A0
FI955775A0 FI955775A FI955775A FI955775A0 FI 955775 A0 FI955775 A0 FI 955775A0 FI 955775 A FI955775 A FI 955775A FI 955775 A FI955775 A FI 955775A FI 955775 A0 FI955775 A0 FI 955775A0
Authority
FI
Finland
Prior art keywords
flow path
substance
reactor
phase
rates
Prior art date
Application number
FI955775A
Other languages
Finnish (fi)
Swedish (sv)
Other versions
FI119919B (en
FI955775A (en
Inventor
George Bodnaras
Original Assignee
Atomaer Pty Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Atomaer Pty Ltd filed Critical Atomaer Pty Ltd
Publication of FI955775A0 publication Critical patent/FI955775A0/en
Publication of FI955775A publication Critical patent/FI955775A/en
Application granted granted Critical
Publication of FI119919B publication Critical patent/FI119919B/en

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/421—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/433—Mixing tubes wherein the shape of the tube influences the mixing, e.g. mixing tubes with varying cross-section or provided with inwardly extending profiles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/433—Mixing tubes wherein the shape of the tube influences the mixing, e.g. mixing tubes with varying cross-section or provided with inwardly extending profiles
    • B01F25/4331—Mixers with bended, curved, coiled, wounded mixing tubes or comprising elements for bending the flow
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/434—Mixing tubes comprising cylindrical or conical inserts provided with grooves or protrusions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J14/00—Chemical processes in general for reacting liquids with liquids; Apparatus specially adapted therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2405—Stationary reactors without moving elements inside provoking a turbulent flow of the reactants, such as in cyclones, or having a high Reynolds-number
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00121—Controlling the temperature by direct heating or cooling
    • B01J2219/0013—Controlling the temperature by direct heating or cooling by condensation of reactants
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00162—Controlling or regulating processes controlling the pressure
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S261/00—Gas and liquid contact apparatus
    • Y10S261/72—Packing elements

Abstract

A multi-phase staged passive reactor (10) for promoting interphasic interaction of a first substance in a liquid phase with a second substance in a non-miscible liquid phase, a solid phase or a gaseous phase. The reactor comprises a plurality of stages (C, D and E) which define a flow path for the substances in different phases. Each stage is shaped to define a substantially curved flow path (12) having a centre of curvature located to one side of the flow path (12). Thus, for example, stages (D) and (E) have a respective centre of curvature (14, 16), on opposite sides of the flow path (12) whereby, in use, as the substances flow through the reactor (10) particles of the second substance are forced to migrate through the first substance, first in one direction and then in substantially the reverse direction due to an inertial field of changing direction thus generated. Due to the differences in the relative densities of the respective phases, differential inertial forces are exerted on each phase as the mixture flows along the general flow direction of the flow path (12) the interphasic interaction thus produced includes both mechanical interaction due to, for example, collisions and energy transfer, as well as chemical reactions due to, for example, oxidation and ion-exchange. There are no moving parts in the reactor (10) which is of relatively simple construction, and it is extremely efficient, achieving high reaction rates, high mass transfer rates and high mixing rates. <IMAGE> <IMAGE>
FI955775A 1993-06-03 1995-11-30 Multiphase stepwise passive reactor FI119919B (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
AUPL918093 1993-06-03
AUPL918093 1993-06-03
PCT/AU1994/000299 WO1994029017A1 (en) 1993-06-03 1994-06-03 Multiphase staged passive reactor
AU9400299 1994-06-03

Publications (3)

Publication Number Publication Date
FI955775A0 true FI955775A0 (en) 1995-11-30
FI955775A FI955775A (en) 1995-12-28
FI119919B FI119919B (en) 2009-05-15

Family

ID=3776945

Family Applications (1)

Application Number Title Priority Date Filing Date
FI955775A FI119919B (en) 1993-06-03 1995-11-30 Multiphase stepwise passive reactor

Country Status (12)

Country Link
US (1) US5741466A (en)
EP (2) EP0701474B1 (en)
JP (1) JP3923514B2 (en)
AT (1) ATE281887T1 (en)
CA (1) CA2164340C (en)
DE (1) DE69434127D1 (en)
FI (1) FI119919B (en)
MY (1) MY110990A (en)
NZ (1) NZ267029A (en)
SG (1) SG46212A1 (en)
WO (1) WO1994029017A1 (en)
ZA (1) ZA943903B (en)

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US7241423B2 (en) * 2000-02-03 2007-07-10 Cellular Process Chemistry, Inc. Enhancing fluid flow in a stacked plate microreactor
US6537506B1 (en) 2000-02-03 2003-03-25 Cellular Process Chemistry, Inc. Miniaturized reaction apparatus
US7056477B1 (en) 2000-02-03 2006-06-06 Cellular Process Chemistry, Inc. Modular chemical production system incorporating a microreactor
US7435392B2 (en) * 2000-02-03 2008-10-14 Acclavis, Llc Scalable continuous production system
US7413714B1 (en) 2000-07-16 2008-08-19 Ymc Co. Ltd. Sequential reaction system
DE10036602A1 (en) * 2000-07-27 2002-02-14 Cpc Cellular Process Chemistry Microreactor for reactions between gases and liquids
BR0116421B1 (en) * 2000-12-21 2011-11-16 bubbler comprising an elevator and a lid.
US7129091B2 (en) * 2002-05-09 2006-10-31 University Of Chicago Device and method for pressure-driven plug transport and reaction
EP1565260B1 (en) * 2002-10-29 2013-10-16 Clean Gas Technologies Ltd. Gas cleaning process and equipment therefor
EP1618372A2 (en) * 2003-04-14 2006-01-25 Cellular Process Chemistry, Inc. System and method for determining optimal reaction parameters using continuously running process
CN1472000A (en) * 2003-06-30 2004-02-04 史汉祥 Improved multiphase reactor
CA2556033C (en) * 2004-02-09 2014-05-13 Indigo Technologies Group Pty Ltd Improved particle interactions in a fluid flow
AT502016B1 (en) * 2005-08-24 2007-01-15 Diehl Hans Juergen SWIRL CHAMBER
SE529516C2 (en) 2005-10-24 2007-09-04 Alfa Laval Corp Ab Universal flow module
WO2007066534A1 (en) * 2005-12-07 2007-06-14 Taiheiyo Cement Corporation Apparatus for removing of unburned carbon from fly ash and relevant removing method
NL2002862C2 (en) * 2009-05-08 2010-11-09 Friesland Brands Bv Microfluidic apparatus and method for generating a dispersion.
DE102010041289B4 (en) * 2009-09-23 2017-09-07 L-Dcs Technology Gmbh Material and heat exchanger plate and a material and heat exchange reactor with such a material and heat exchanger plate
WO2014193260A1 (en) * 2013-05-29 2014-12-04 Gubenko Lev Anatolyevich Method and device for extruding plasticized powdered materials (variants)
GB201703299D0 (en) * 2017-03-01 2017-04-12 Triple Line Tech Ltd Apparatus and method for generating a microfoam

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DE522673C (en) * 1925-08-26 1931-04-13 Hermann Hildebrandt Device for mixing, atomizing or gasifying all kinds of substances
DE1059888B (en) * 1957-11-30 1959-06-25 Degussa Method and device for carrying out an exchange of substance and / or heat between gaseous and / or liquid media
US3388893A (en) * 1962-03-23 1968-06-18 Raymond C. Hall Material handling device
FR1461788A (en) * 1964-12-02 1966-12-09 Method and device for spraying a liquid and its intimate mixing with gases
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US3856270A (en) * 1973-10-09 1974-12-24 Fmc Corp Static fluid mixing apparatus
DE2518975C3 (en) * 1975-04-29 1980-07-31 Dynamit Nobel Ag, 5210 Troisdorf Device for carrying out direct current reactions in heterogeneous systems
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IT1129126B (en) * 1980-08-01 1986-06-04 Fiat Ricerche HIGH CAPACITY DEVICE FOR THE PREPARATION OF A MIXTURE INCLUDING A SOLID PHASE AND A LIQUID PHASE OF A METAL ALLOY
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Also Published As

Publication number Publication date
CA2164340A1 (en) 1994-12-22
JP3923514B2 (en) 2007-06-06
EP0701474A4 (en) 1996-06-26
JPH09504466A (en) 1997-05-06
ATE281887T1 (en) 2004-11-15
EP1405667A2 (en) 2004-04-07
EP1405667A3 (en) 2004-06-30
DE69434127D1 (en) 2004-12-16
FI119919B (en) 2009-05-15
EP0701474B1 (en) 2004-11-10
EP0701474A1 (en) 1996-03-20
SG46212A1 (en) 1998-02-20
CA2164340C (en) 2005-03-22
ZA943903B (en) 1995-02-02
FI955775A (en) 1995-12-28
WO1994029017A1 (en) 1994-12-22
MY110990A (en) 1999-07-31
US5741466A (en) 1998-04-21
NZ267029A (en) 1997-03-24

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